CN107569979A - A kind of structures and methods for eliminating absorption tower exit sharp pounding - Google Patents

A kind of structures and methods for eliminating absorption tower exit sharp pounding Download PDF

Info

Publication number
CN107569979A
CN107569979A CN201710868170.5A CN201710868170A CN107569979A CN 107569979 A CN107569979 A CN 107569979A CN 201710868170 A CN201710868170 A CN 201710868170A CN 107569979 A CN107569979 A CN 107569979A
Authority
CN
China
Prior art keywords
absorption tower
exhaust pass
deflector
spacing
sharp pounding
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201710868170.5A
Other languages
Chinese (zh)
Inventor
史绍平
穆延非
闫姝
张波
陈新明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Huaneng Clean Energy Research Institute
China Huaneng Group Co Ltd
Original Assignee
Huaneng Clean Energy Research Institute
China Huaneng Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Huaneng Clean Energy Research Institute, China Huaneng Group Co Ltd filed Critical Huaneng Clean Energy Research Institute
Priority to CN201710868170.5A priority Critical patent/CN107569979A/en
Publication of CN107569979A publication Critical patent/CN107569979A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

A kind of structure for eliminating absorption tower exit sharp pounding, in IGCC power stations, cos (COS) in former synthesis gas are absorbed by hydrolysis absorption tower, former synthesis gas is entered in tower by inlet flue duct, ultimately form net synthesis gas by demister, flue demister, exhaust pass in pallet, absorbed layer, tower successively from down to up.Because absorption tower exhaust pass and tower body are in 90 ° of arrangements, and flue demister cross-sectional area is larger, and absorption tower exit is in bell shape, so absorption tower exit easily produces an air flow swirl, so as to trigger sharp pounding.The present invention by exhaust pass horn mouth position be provided with it is some to gas rise guide functions nonuniform mutation operator deflectors, the air flow swirl at the horn mouth of absorption tower exit can be eliminated, so as to eliminate vibrations, not only easy to implement but also positive effect, COS hydrolysis efficiencies can be provided simultaneously, the overall pressure drop on absorption tower can also be reduced, saves energy consumption.

Description

A kind of structures and methods for eliminating absorption tower exit sharp pounding
Technical field
It is more particularly to a kind of to eliminate absorption tower the invention belongs to synthesis gas COS hydrolysis process technical fields in IGCC power stations The structures and methods of exit sharp pounding.
Background technology
In IGCC power stations, the desulfurization of gasification furnace exiting syngas, mainly absorbed by hydrolysis method in synthesis gas Cos (COS).The height relative diameter on absorption tower is very big, is in the form of a column.Increase flue demister in the exit on absorption tower, COS absorption efficiencies can further be improved.Because the cross-sectional area of absorption tower outlet is less than the cross-sectional area of flue demister, institute Bell-mouthed shape has been made with the outlet on absorption tower.Due to bell-mouthed presence so that flow field is unstable in the presence of one herein Synthesis gas whirlpool, so as to not only increase the pressure drop on absorption tower, and the strong vibrations in absorption tower can be caused, or even can cause Serious accident.
The content of the invention
The shortcomings that in order to overcome above-mentioned prior art, it is strong to eliminate absorption tower exit it is an object of the invention to provide one kind The dynamic structures and methods of violent shock, by setting guiding device in the exit on absorption tower, for eliminating gas swirl, solve above-mentioned Problem.
To achieve these goals, the technical solution adopted by the present invention is:
A kind of structure for eliminating absorption tower exit sharp pounding, the outlet on absorption tower 2 are in bell shape, exhaust pass 8 with the tower body of absorption tower 2 in 90 ° arrangement, in exhaust pass 8 horn mouth position be provided with it is some to gas rise guide functions lead Flowing plate 6.
The deflector 6 is made or in surface spraying anti-corrosion material using anti-corrosion material.
The deflector 6 sets 3~6 groups from top to bottom, and every group is made up of according to mounting condition polylith.
Micro gap is left between the deflector 6 and between deflector 6 and the side wall of exhaust pass 8.
The deflector 6 is divided into horizontal segment and empennage section along synthesis gas flow direction, and the length of horizontal segment is with exporting cigarette The entrance horizontal segment in road 8 is identical, and empennage segment length is 0.1L2~0.2L2, L parallel with the horn mouth side of exhaust pass 82It is The entrance horizontal section length of exhaust pass 8 and oared segrne pii length sum.
The horizontal segment of spacing and deflector 6 between the horizontal segment of the deflector 6 and the entrance of exhaust pass 8 are horizontal Section side wall spacing is nonuniform mutation operator, and spacing above is small, and spacing below is big.Uppermost spacing, i.e. the superiors' deflector 6 It is minimum spacing h with the spacing of side wall on exhaust pass 81, h1=0.1L1~0.2L1, nethermost spacing, i.e. orlop are led The spacing of flowing plate 6 and the lower side wall of exhaust pass 8, it is maximum spacing h5, h5=0.3L1~0.4L1, L1It is the minimum of exhaust pass 8 Diameter, i.e. horn inlet diameter, namely the entrance horizontal segment diameter of exhaust pass 8.
The empennage elongated segment line of the deflector 6 to the spacing between the horn outlet intersection of exhaust pass 8 is uniform Arrangement.
The absorption tower 2 enters absorption tower including inlet flue duct 1, successively by demister 5 in pallet 3, absorbed layer 4, tower, Flue demister 7 and exhaust pass 8, former synthesis gas enter tower body by inlet flue duct 1, successively by pallet 3, absorbed layer 4, tower Demister 5, deflector 6, flue demister 7 and exhaust pass 8, ultimately form net synthesis gas and arrange to air.
The present invention eliminates the method for absorption tower exit sharp pounding, the guide functions using deflector 6 to gas, eliminates The whirlpool of gas flowing, so as to solve vibration problems.
Compared with prior art, the present invention is capable of the gas flowfield in reasonable distribution absorption tower exit, can be completely eliminated Air flow swirl at the horn mouth of absorption tower exit, shaken so as to eliminate, not only easy to implement but also positive effect, while can COS hydrolysis efficiencies are provided, the overall pressure drop on absorption tower can also be reduced, save energy consumption.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention.
Fig. 2 is the layout drawing of deflector.
Fig. 3 is the flow field at horn mouth before transforming.
Fig. 4 is to increase the flow field after deflector at horn mouth.
Fig. 5 is to increase the overall simulation design sketch after deflector.
Embodiment
Describe embodiments of the present invention in detail with reference to the accompanying drawings and examples.
As shown in figure 1, a kind of structure chart for eliminating the vibrations of absorption tower exit, former synthesis gas is entered by inlet flue duct 1 to be inhaled Tower tower body is received, successively by demister 5, deflector 6, flue demister 7 in pallet 3, absorbed layer 4, tower, finally by exhaust pass 8 rows are to air.Because exhaust pass 8 and tower body are in 90 ° of arrangements, and the cross-sectional area of flue demister 7 is larger, absorption tower exit In bell shape, so absorption tower exit easily produces a gas swirl, so as to trigger sharp pounding.
By simulation it can be seen that the whirlpool in absorption tower exit is as shown in Figure 3.The position of gas swirl as can be seen from Figure 3 Put mainly in horn mouth, caused by being primarily due to gas velocity skewness, flow velocity of the gas on top is higher, bottom Flow velocity is relatively low.
Then according to size distribution of the gas in cross section, the deflector group of nonuniform mutation operator is designed, typically from top to bottom 3~6 groups are set, every group can be made up of according to mounting condition polylith, and deflector 6 is made or prevented in surface spraying using anti-corrosion material Rotten material.Micro gap is left between deflector 6 and between deflector 6 and the side wall of exhaust pass 8.
The deflector 6 designed according to Fig. 3 is as shown in Figure 2.It can divide a horizontal segment and empennage section along gas flow direction.Water The length of flat section is identical with respective horizontal flue, and empennage segment length is 0.1L2~0.2L2
To cause the gas velocity in absorption tower exit uniform, the spacing for setting deflector horizontal segment is nonuniform mutation operator, Spacing above is small, and spacing below is big, uppermost spacing, i.e. minimum spacing h1, typically it is dimensioned to 0.1L1~ 0.2L1, nethermost spacing, i.e. maximum spacing h5, typically it is dimensioned to 0.3L1~0.4L1;The empennage Duan Yan of deflector Long line is to be evenly arranged to the spacing between horizontal flue demister entrance intersection, i.e. spacing h0It is equal.
The absorption tower flow field for adding deflector is simulated, as a result as shown in figure 4, in absorption tower exit, water conservancy diversion Plate 6 is reasonably assigned with synthesis tolerance, and gas flowing whirlpool is wholly absent.
The overall flow field design sketch in the absorption tower exit after deflector is added as shown in figure 5, gas flowfield uniformly divides Cloth, and the pressure drop on absorption tower significantly reduces, while COS hydrolysis efficiencies, significant effect can be provided.

Claims (10)

1. a kind of structure for eliminating absorption tower exit sharp pounding, the outlet of absorption tower (2) is in bell shape, exhaust pass (8) with absorption tower (2) tower body in 90 ° of arrangements, it is characterised in that horn mouth position is provided with some right in exhaust pass (8) Gas plays the deflector (6) of guide functions.
2. the structure of absorption tower exit sharp pounding is eliminated according to claim 1, it is characterised in that the deflector (6) it is made or in surface spraying anti-corrosion material using anti-corrosion material.
3. the structure of absorption tower exit sharp pounding is eliminated according to claim 1, it is characterised in that the deflector (6) 3~6 groups are set from top to bottom, and every group is made up of according to mounting condition polylith.
4. the structure of absorption tower exit sharp pounding is eliminated according to claim 3, it is characterised in that the deflector (6) micro gap is left between and between deflector (6) and exhaust pass (8) side wall.
5. according to the structure for eliminating absorption tower exit sharp pounding of claim 1 or 3, it is characterised in that the water conservancy diversion Plate (6) is divided into horizontal segment and empennage section along synthesis gas flow direction, and the length of horizontal segment is horizontal with the entrance of exhaust pass (8) Duan Xiangtong, empennage segment length are 0.1L2~0.2L2, L parallel with the horn mouth side of exhaust pass (8)2It is exhaust pass (8) Entrance horizontal section length and oared segrne pii length sum.
6. the structure of absorption tower exit sharp pounding is eliminated according to claim 5, it is characterised in that the deflector (6) spacing between horizontal segment and the horizontal segment of deflector (6) and the entrance horizontal segment side wall spacing of exhaust pass (8) are Nonuniform mutation operator, spacing above is small, and spacing below is big.
7. the structure of absorption tower exit sharp pounding is eliminated according to claim 6, it is characterised in that uppermost Away from the spacing of side wall that is, on the superiors' deflector (6) and exhaust pass (8), is minimum spacing h1, h1=0.1L1~0.2L1, most Following spacing, the i.e. spacing of orlop deflector (6) and exhaust pass (8) lower side wall, it is maximum spacing h5, h5=0.3L1~ 0.4L1, L1It is the minimum diameter of exhaust pass (8), i.e. horn inlet diameter, namely the entrance horizontal segment of exhaust pass (8) are straight Footpath.
8. the structure of absorption tower exit sharp pounding is eliminated according to claim 6, it is characterised in that the deflector (6) empennage elongated segment line is to be evenly arranged to the spacing between the horn outlet intersection of exhaust pass (8).
9. the structure of absorption tower exit sharp pounding is eliminated according to claim 1, it is characterised in that the absorption tower (2) absorption tower is entered including inlet flue duct (1), successively by demister (5), flue demisting in pallet (3), absorbed layer (4), tower Device (7) and exhaust pass (8), former synthesis gas enter tower body by inlet flue duct (1), successively by pallet (3), absorbed layer (4), tower Interior demister (5), deflector (6), flue demister (7) and exhaust pass (8), ultimately form net synthesis gas and arrange to air.
10. a kind of method for eliminating absorption tower exit sharp pounding, the outlet of absorption tower (2) is in bell shape, exports cigarette Road (8) is with absorption tower (2) tower body in 90 ° of arrangements, it is characterised in that horn mouth position sets some lead in exhaust pass (8) Flowing plate (6), the guide functions using deflector (6) to gas, the whirlpool that gas flows is eliminated, so as to solve vibration problems.
CN201710868170.5A 2017-09-22 2017-09-22 A kind of structures and methods for eliminating absorption tower exit sharp pounding Pending CN107569979A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710868170.5A CN107569979A (en) 2017-09-22 2017-09-22 A kind of structures and methods for eliminating absorption tower exit sharp pounding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710868170.5A CN107569979A (en) 2017-09-22 2017-09-22 A kind of structures and methods for eliminating absorption tower exit sharp pounding

Publications (1)

Publication Number Publication Date
CN107569979A true CN107569979A (en) 2018-01-12

Family

ID=61038698

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710868170.5A Pending CN107569979A (en) 2017-09-22 2017-09-22 A kind of structures and methods for eliminating absorption tower exit sharp pounding

Country Status (1)

Country Link
CN (1) CN107569979A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202146712U (en) * 2011-06-27 2012-02-22 南京龙源环保有限公司 Smoke catalytic reduction denitration device capable of mixing uniformly, equalizing and guiding flow
CN104740993A (en) * 2015-04-13 2015-07-01 中电投远达环保工程有限公司 Three-stage zoned collaborative dust removal and desulfurization system

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202146712U (en) * 2011-06-27 2012-02-22 南京龙源环保有限公司 Smoke catalytic reduction denitration device capable of mixing uniformly, equalizing and guiding flow
CN104740993A (en) * 2015-04-13 2015-07-01 中电投远达环保工程有限公司 Three-stage zoned collaborative dust removal and desulfurization system

Similar Documents

Publication Publication Date Title
CN105749690B (en) Promote the device and method that fine particle interacts in fire coal boiler fume
CN105597477A (en) Device and method for removing ultrafine particles in flue gas of coal boiler
CN205517227U (en) Desulfurizing tower suitable for ultra -clean discharges
CN207628210U (en) A kind of dry desulfurization denitration reaction tower gas approach structure and flue gas flow guiding device
CN107952292A (en) A kind of efficient demisting coalescer of flux adjustable venturi-eddy flow coupled mode
CN108939755A (en) Ship tail gas desulfurizer
CN106076076A (en) A kind of liquid distributor
CN105797582B (en) A kind of the differentiation spray ammonia reactor and spray ammonia method of SCR denitration
CN107158910A (en) A kind of denitrating flue gas ozone reaction device
CN207287071U (en) A kind of structure for eliminating absorption tower exit sharp pounding
CN207187488U (en) A kind of double ultra-clean desulfurized dust collection columns of spray of the double turbulent flows of single cycle
CN107569979A (en) A kind of structures and methods for eliminating absorption tower exit sharp pounding
CN202105573U (en) Novel unevenly porous air distribution plate
CN205598871U (en) Fine particles interact's device in promotion coal fired boiler flue gas
CN106237724A (en) A kind of sound wave coupled rotational flow racemization high-effective dust-removing demister
CN207741581U (en) A kind of flue gas water conservancy diversion spraying ventilating device
CN204159160U (en) Modified Water Screen Duster of Cupola
CN208627053U (en) A kind of coal gasifying process gasifying agent mixing arrangement
CN206577907U (en) A kind of airflow uniform distribution applied to wet electrical dust precipitator entrance is combined the unit
CN201832553U (en) Smoke gas jet bubbling blasting desulphurization tower
CN201906563U (en) n-shaped cold model experiment device for flue gas denitration
CN202054810U (en) Wet desulfurizer for methane desulfurization
CN204816193U (en) Flue gas guiding device on desulfurization absorption tower
CN203043807U (en) Device for making sulfuric acid used for regulating cooling circulating water by utilizing furnace smoke of boiler
CN106622660A (en) Side outlet type wet electrostatic precipitator

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20180112

WD01 Invention patent application deemed withdrawn after publication